CN202472448U - Automatic temperature control system of aqueous solution dye production - Google Patents
Automatic temperature control system of aqueous solution dye production Download PDFInfo
- Publication number
- CN202472448U CN202472448U CN2011205166522U CN201120516652U CN202472448U CN 202472448 U CN202472448 U CN 202472448U CN 2011205166522 U CN2011205166522 U CN 2011205166522U CN 201120516652 U CN201120516652 U CN 201120516652U CN 202472448 U CN202472448 U CN 202472448U
- Authority
- CN
- China
- Prior art keywords
- temperature
- module
- control system
- temperature detecting
- detecting module
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Control Of Temperature (AREA)
Abstract
The utility model provides an automatic temperature control system of an aqueous solution dye production, comprising a temperature detection module 1, a temperature detection module 2, a temperature detection module 3, a temperature integrated data module, a main control system module and a feed system module. In allusion to an automatic temperature control device of the aqueous solution dye production, the utility model designs the independent control system, so that accurate detection information and operation command can be obtained, the automation operation is conducive to realize, the accurate control of reaction condition and the product quality can be guaranteed, and the product yield is conducive to improve.
Description
Technical field
The utility model relates to water-soluble dye production equipment control system field, is specifically related to the automatic temperature control system that a kind of aqueous dyestuff is produced.
Background technology
In the reactive dye production run, often need cooling on the rocks or feed steam to heat up, in the reasonable scope with the temperature of reaction of guaranteeing material.In summer high temperature period, the processing if material is in time lowered the temperature causes the mixture temperature value of overruning, and has greatly influenced the end product quality of water-soluble dye.For guaranteeing that material is in stable low-temperature condition, in the very high frequency of cooling on the rocks in summer, adopt workload artificial on the rocks very big, form the manpower requirement peak in the short time, also be unfavorable for the reasonable distribution that the worker measures.Simultaneously, the adjustment of reasonable temperature depends on the correct judgement to reactor temperature; And the obtaining of reactor temperature value; What the general sample bucket sampling and measuring that adopts, the sampling that obtains through this kind method depended on sample bucket fully goes into the still degree of depth, and situation is changeable in the agitated reactor; So the numerical value that existing method is measured is unstable, error is big.Therefore operating personnel can't carry out temperature control work according to Temperature numerical accurately, so yield of product that obtains and quality all are difficult to assurance.
The utility model content
The automatic temperature control system that the utility model provides a kind of and measured accurately, reinforced aqueous dyestuff is accurately produced.
The utility model is realized through following technical scheme:
The automatic temperature control system that aqueous dyestuff is produced comprises:
In order to the temperature detecting module one of agitated reactor inner bottom part potpourri being carried out temperature detection,
In order to the temperature detecting module two of agitated reactor inner bottom part potpourri being carried out temperature detection,
In order to the temperature detecting module three of agitated reactor inner bottom part potpourri being carried out temperature detection,
Be used for according to temperature detecting module one detect numerical value, temperature detecting module two detect numerical value and temperature detecting module three detect temperature integrated data module that numerical value obtain weighted average increment,
Be used for the numeric ratio of temperature integrated data module according to the temperature adjusting range values, need to determine whether the master control system module that carry out temperature adjusting on the rocks,
And the order on the rocks that is used to receive the master control system module, the feed system module of agitated reactor being carried ice block cooling;
The signal output part of wherein said temperature detecting module one is connected with a signal input part of temperature integrated data module;
The signal output part of said temperature detecting module two is connected with a signal input part of temperature integrated data module;
The signal output part of said temperature detecting module three is connected with a signal input part of temperature integrated data module;
The signal output part of said temperature integrated data module is connected with the signal input part of master control system module;
The signal output part of said master control system module is connected with the signal input part of feed system module.
The beneficial effect of the utility model is: the automatic temp controller to aqueous dyestuff production designs independently control system; Can obtain and detect information and operational order accurately; Be beneficial to the realization of automation mechanized operation; Can guarantee accurate control, help to improve product yield and guarantee product quality reaction conditions.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Among the figure: 1 is temperature detecting module one; 2 is temperature detecting module two; 3 is temperature detecting module three; 4 is temperature integrated data module; 5 is the master control system module; 6 is the feed system module.
Embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is explained further details.
The automatic temperature control system that the utility model provides a kind of aqueous dyestuff to produce; Comprise: in order to the temperature detecting module 1 of agitated reactor inner bottom part potpourri being carried out temperature detection, in order to the temperature detecting module 22 of middle part potpourri in the agitated reactor being carried out temperature detection, in order to agitated reactor internal upper part potpourri being carried out the temperature detecting module 33 of temperature detection, more than three temperature detecting module obtain obtain still at the bottom of, the temperature detection data in the still, on the still.Above data will be summarized in temperature integrated data module 4, obtain the mean values of weighting, be the mean value of temperature in the kettle, and this numerical value precision is higher, and the desirable degree that is used for temperature adjusting is stronger.The weighted average increment that master control system module 5 is obtained according to temperature integrated data module 4 again is according to the temperature adjusting range values of setting in the system, need to determine whether the temperature adjusting that carries out on the rocks.If do not need on the rocks, then signal finally this.On the rocks if desired, then receive the order on the rocks of master control system module 5 by feed system module 6, agitated reactor is carried ice block cooling.
In the utility model, the signal output part of temperature detecting module 1, temperature detecting module 22 and temperature detecting module 33 is connected with three signal input parts of temperature integrated data module 4 respectively; And the signal output part of temperature integrated data module 4 is connected with the signal input part of master control system module 5; The signal output part of master control system module 5 is connected with the signal input part of feed system module 6.
The utility model designs independently control system to the automatic temp controller of aqueous dyestuff production; Can obtain and detect information and operational order accurately; Be beneficial to the realization of automation mechanized operation, can guarantee accurate control, help to improve product yield and guarantee product quality reaction conditions.
Claims (1)
1. the automatic temperature control system produced of aqueous dyestuff is characterized in that said system comprises:
In order to the temperature detecting module one of agitated reactor inner bottom part potpourri being carried out temperature detection,
In order to the temperature detecting module two of agitated reactor inner bottom part potpourri being carried out temperature detection,
In order to the temperature detecting module three of agitated reactor inner bottom part potpourri being carried out temperature detection,
Be used for according to temperature detecting module one detect numerical value, temperature detecting module two detect numerical value and temperature detecting module three detect temperature integrated data module that numerical value obtain weighted average increment,
Be used for the numeric ratio of temperature integrated data module according to the temperature adjusting range values, need to determine whether the master control system module that carry out temperature adjusting on the rocks,
And the order on the rocks that is used to receive the master control system module, the feed system module of agitated reactor being carried ice block cooling;
The signal output part of wherein said temperature detecting module one is connected with a signal input part of temperature integrated data module;
The signal output part of said temperature detecting module two is connected with a signal input part of temperature integrated data module;
The signal output part of said temperature detecting module three is connected with a signal input part of temperature integrated data module;
The signal output part of said temperature integrated data module is connected with the signal input part of master control system module;
The signal output part of said master control system module is connected with the signal input part of feed system module.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205166522U CN202472448U (en) | 2011-12-12 | 2011-12-12 | Automatic temperature control system of aqueous solution dye production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205166522U CN202472448U (en) | 2011-12-12 | 2011-12-12 | Automatic temperature control system of aqueous solution dye production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202472448U true CN202472448U (en) | 2012-10-03 |
Family
ID=46920592
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205166522U Expired - Fee Related CN202472448U (en) | 2011-12-12 | 2011-12-12 | Automatic temperature control system of aqueous solution dye production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202472448U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104907024A (en) * | 2015-05-13 | 2015-09-16 | 萧山工业研究院 | Control method of chemical reaction vessel full-automatic ice adding device |
-
2011
- 2011-12-12 CN CN2011205166522U patent/CN202472448U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104907024A (en) * | 2015-05-13 | 2015-09-16 | 萧山工业研究院 | Control method of chemical reaction vessel full-automatic ice adding device |
| CN104907024B (en) * | 2015-05-13 | 2016-08-17 | 萧山工业研究院 | Chemical reaction kettle automatically adds the control method of ice production apparatus |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203101933U (en) | Aquiculture water quality on-line monitoring system based on Internet of Things | |
| CN101748477B (en) | Intelligent PID control method for controlling growth process of monocrystalline silicon and system thereof | |
| CN104808587A (en) | Utilization statistical approach based on operation states of machining equipment | |
| CN101706493A (en) | On-line water quality monitoring method of aquaculture ponds and system | |
| CN104020800A (en) | Online dyeing feedback control system and method | |
| CN102621032A (en) | Automatic tester for gas content in coal gas | |
| CN202255665U (en) | Novel thermocouple temperature measurement module | |
| CN104686079A (en) | Cutting platform height automatic control system based on electro-hydraulic control | |
| CN110702735A (en) | Residual chlorine electrode calibration method and water quality detection instrument | |
| CN202472448U (en) | Automatic temperature control system of aqueous solution dye production | |
| CN104932367A (en) | Greenhouse multi-point and multi-parameter detector based on Android intelligent device and detection method | |
| CN202033673U (en) | Automatic PH (potential hydrogen) value adjusting system for fermentation tank | |
| CN101598927A (en) | A kind of soda carbonization technique control system and control method thereof based on neural network | |
| CN201945339U (en) | Gas-liquid two-phase flow online monitoring and metering device | |
| CN202453749U (en) | Automatic feeding control system for aqueous-solution dye production | |
| CN201819724U (en) | Battery injection weighing system | |
| CN202057594U (en) | Coke oven heating coal charge moisture online measuring system | |
| CN204679450U (en) | A kind of Binder Materials type supersonic monitor | |
| CN204189017U (en) | A kind of marsh gas fermentation processes condition detecting system | |
| CN102262010B (en) | Method for testing chemical titer of chlorotetracycline fermentation liquor | |
| CN205014975U (en) | Continuous type pumped storage unit axis measurement system | |
| CN205478257U (en) | Pump efficiency, flow and lift detecting system | |
| CN202453337U (en) | Device for detecting pH value of reaction kettle for producing aqueous solution dyes | |
| CN202453093U (en) | Device for detecting temperature in water soluble dye production reaction kettle | |
| CN201301296Y (en) | Rosin size producing device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121003 Termination date: 20141212 |
|
| EXPY | Termination of patent right or utility model |